Desenvolvimento de membranas catalíticas ácidas para a metanólise do ácido palmítico: estudo do efeito da reticulação

A produção de biodiesel tem sido afectada, ao nível dos custos de produção, pela falta de matérias-primas adequadas que não entrem em competição com a indústria alimentar. A matéria-prima original para a produção de biodiesel é o óleo de soja alimentar, porém a sua utilização origina problemas significativos a nível político e económico. Desta forma, a indústria do biodiesel encontra-se empenhada na modificação para matériasprimas alternativas e de baixo custo. Contudo, estas matérias-primas apresentam elevados níveis de ácidos gordos livres, sendo por isso necessária a eliminação dos ácidos gordos livres. Neste trabalho experimental é proposta a metanólise do ácido palmítico catalisada por membranas poliméricas catalíticas ácidas, utilizadas num reactor de membrana com pervaporação simultânea. Este processo é uma alternativa á destilação reactiva visto que permite a integração da reacção e da separação numa única operação, pelo que é possível a optimização energética, a maximização da conversão e a eliminação de solventes de extracção. Foi efectuado o estudo cinético da reacção de esterificação catalisada pelo catalisador KIT-6 sulfonado. Este catalisador foi caracterizado por titulação ácido-base. Prepararam-se membranas catalíticas compósitas por dispersão do KIT-6 sulfonado em matrizes de poli(álcool vinílico) reticulado com glutaraldeído ou hexametilenodiisocianato. As membranas foram caracterizadas por medição de ângulos de contacto, percentagem de inchamento e por FTIR. Os efeitos do tipo de reticulante e da percentagem de reticulação nas propriedades de transporte e de sorção das membranas, foram estudados em reactor bacth, com as membranas cortadas em pedaços. Os elevados períodos de indução apresentados pelas curvas cinéticas obtidas sugerem que a água formada na reacção afecta de forma pronunciada as propriedades de transporte das membranas. Esta hipótese foi suportada pelo bom ajuste dum modelo cinético-difusional aos pontos experimentais. Por fim, foi testada uma membrana em reactor de membrana com pervaporação simultânea, utilizando azoto seco como gás de varrimento.

The thermal effects on the methanol-to-olefins reaction: A modelling and experimental approach

With the projection of an increasing world population, hand-in-hand with a journey towards a bigger number of developed countries, further demand on basic chemical building blocks, as ethylene and propylene, has to be properly addressed in the next decades. The methanol-to-olefins (MTO) is an interesting reaction to produce those alkenes using coal, gas or alternative sources, like biomass, through syngas as a source for the production of methanol. This technology has been widely applied since 1985 and most of the processes are making use of zeolites as catalysts, particularly ZSM-5. Although its selectivity is not especially biased over light olefins, it resists to a quick deactivation by coke deposition, making it quite attractive when it comes to industrial environments; nevertheless, this is a highly exothermic reaction, which is hard to control and to anticipate problems, such as temperature runaways or hot-spots, inside the catalytic bed. The main focus of this project is to study those temperature effects, by addressing both experimental, where the catalytic performance and the temperature profiles are studied, and modelling fronts, which consists in a five step strategy to predict the weight fractions and activity. The mind-set of catalytic testing is present in all the developed assays. It was verified that the selectivity towards light olefins increases with temperature, although this also leads to a much faster catalyst deactivation. To oppose this effect, experiments were carried using a diluted bed, having been able to increase the catalyst lifetime between 32% and 47%. Additionally, experiments with three thermocouples placed inside the catalytic bed were performed, analysing the deactivation wave and the peaks of temperature throughout the bed. Regeneration was done between consecutive runs and it was concluded that this action can be a powerful means to increase the catalyst lifetime, maintaining a constant selectivity towards light olefins, by losing acid strength in a steam stabilised zeolitic structure. On the other hand, developments on the other approach lead to the construction of a raw basic model, able to predict weight fractions, that should be tuned to be a tool for deactivation and temperature profiles prediction.

Valorization of olive pomace through combination of biocatalysis with supercritical fluid technology

A supercritical carbon dioxide (scCO2) based oil extraction method was implemented on olive pomace (alperujo), and an oil yield of 25,5 +/- 0,8% (goil/gdry residue) was obtained. By Soxhlet extraction with hexane, an oil extraction yield of 28,9 +/- 0,8 % was obtained, which corresponds to an efficiency of 88,4 +/- 4,8 % for the supercritical method. The scCO2 extraction process was optimized for operating conditions of 50 MPa and 348,15 K, for which an oil loading of 32,60 g oil/kg CO2 was calculated. As a proof of concept, olive pomace was used as feedstock for biodiesel production, in a process combining the use of lipase as a catalyst with the use of scCO2 as a solvent, and integrating the steps of oil extraction, oil to biodiesel transesterification and subsequent separation of the latter. In the conducted experiments, FAME (fatty acid methyl ester) purities of 90% were obtained, with the following operating parameters: an oil:methanol molar ratio of 1:24; a residence time of 7,33 and 11,6 mins; a pressure of 40 MPa; a temperature of 313,15 K; and Lipozyme (Mucor miehei; Sigma-Aldritch) as an enzyme. However, oscillations of FAME purity were registered throughout the experiments, which could possibly be due to methanol accumulation in the enzymatic reactor. Finally, the phenolic content of olive pomace, and the effect of the drying process – oven or freeze-drying – and the extraction methods – hydro-alcoholic method and supercritical method – on the phenolic content were analysed. It was verified that the oven-drying process on the olive pomace preserved 90,1 +/- 3,6 % of the total phenolic content. About 62,3 +/- 5,53% of the oven-dried pomace phenolic content was extracted using scCO2 at 60 MPa and 323,15 K. Seven individual phenols – hydroxytyrosol, tyrosol, oleuropein, quercetin, caffeic acid, ferulic acid and p-coumaric acid – were identified and quantified by HPLC.

Impact of carbon/nitrogen feeding strategy on polyhydroxyalkanoates production using mixed microbial cultures

Polyhydroxyalkanoates (PHA) production using mixed microbial cultures (MMC) requires a multi-stage process involving the microbial selection of PHA-storing microorganisms, typically operated in sequencing batch reactors (SBR), and an accumulation reactor. Since low-cost renewable feedstocks used as process feedstock are often nitrogen-deficient, nutrient supply in the selection stage is required to allow for microbial growth. In this context, the possibility to uncouple nitrogen supply from carbon feeding within the SBR cycle has been investigated in this study. Moreover, three different COD:N ratios (100:3.79, 100:3.03 and 100:2.43) were tested in three different runs which also allowed the study of COD:N ratio on the SBR performance. For each run, a synthetic mixture of acetic and propionic acids at an overall organic load rate of 8.5 gCOD L-1 d-1 was used as carbon feedstock, whereas ammonium sulfate was the nitrogen source in a lab-scale sequence batch reactor (SBR) with 1 L of working volume. Besides, a sludge retention time (SRT) of 1 d was used as well as a 6 h cycle length. The uncoupled feeding strategy significantly enhanced the selective pressure towards PHA-storing microorganisms, resulting in a two-fold increase in the PHA production (up to about 1.3 gCOD L-1). A high storage response was observed for the two runs with the COD:N ratios (gCOD:gN) of 100:3.79 and 100:3.03, whereas the lowest investigated nitrogen load resulted in very poor performance in terms of polymer production. In fact, strong nitrogen limitation caused fungi to grow and a very poor storage ability by microorganisms that thrived in those conditions. The COD:N ratio also affected the polymer composition, indeed the produced poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) showed a variable HV content (1-20 %, w/w) among the three runs, lessening as the COD:N increased. This clearly suggests the possibility to use the COD:N ratio as a tool for tuning polymer properties regardless the composition of the feedstock.

Coupling organic substrate removal to methane production in a fully biological microbial electrolysis cell

Microbial electrolysis cells (MECs) are an innovative and emerging technique based on the use of solid-state electrodes to stimulate microbial metabolism for wastewater treatment and simultaneous production of value-added compounds (such as methane). This research studied the performance of a two-chamber MEC in terms of organic matter oxidation (at the anode) and methane production (at the cathode). MEC‟s anode had been previously inoculated with an activated sludge, whereas the cathode chamber inoculum was an anaerobic sludge (containing methanogenic microorganisms). During the experimentation, the bioanode was continuously fed with synthetic solutions in anaerobic basal medium, at an organic load rate (OLR) of around 1 g L-1 d-1, referred to the chemical oxygen demand (COD). At the beginning (Run I), the feeding solution contained acetate and subsequently (Run II) it was replaced with a more complex solution containing soluble organic compounds other than acetate. For both conditions, the anode potential was controlled at -0.1 V vs. standard hydrogen electrode, by means of a potentiostat. During Run I, over 80% of the influent acetate was anaerobically oxidized at the anode, and the resulting electric current was recovered as methane at the cathode (with a cathode capture efficiency, CCE, accounting around 115 %). The average energy efficiency of the system (i.e., the energy captured into methane relative to the electrical energy input) under these conditions was over 170%. However, reactor‟s performance decreased over time during this run. Throughout Run II, a substrate oxidation over 60% (on COD basis) was observed. The electric current produced (57% of coulombic efficiency) was also recovered as methane, with a CCE of 90%. For this run the MEC‟s average energy efficiency accounted for almost 170 %. During all the experimentation, a very low biomass growth was observed at the anode whereas ammonium was transferred through the cationic membrane and concentrated at the cathode. Tracer experiments and scanning electron microscopy analyses were also carried out to gain a deeper insight into the reactor performance and also to investigate the possible reasons for partial loss of performance. In conclusion, this research suggests the great potential of MEC to successfully treat low-strength wastewaters, with high energy efficiency and very low sludge production.

Therapeutics bioconjugates: evaluation of iminoboronates as payload delivery system for cancer

The advent of bioconjugation impacted deeply the world of sciences and technology. New biomolecules were found, biological processes were understood, and novel methodologies were formed due to the fast expansion of this area. The possibility of creating new effective therapies for diseases like cancer is one of big applications of this now big area of study. Off target toxicity was always the problem of potent small molecules with high activity towards specific tumour targets. However, chemotherapy is now selective due to powerful linkers that connect targeting molecules with affinity to interesting biological receptors and cytotoxic drugs. This linkers must have very specific properties, such as high stability in plasma, no toxicity, no interference with ligand affinity nor drug potency, and at the same time, be able to lyse once inside the target molecule to release the therapeutic warhead. Bipolar environments between tumour intracellular and extracellular medias are usually exploited by this linkers in order to complete this goal. The work done in this thesis explores a new model for that same task, specific cancer drug delivery. Iminoboronates were studied due to its remarkable selective stability towards a wide pH range and endogenous molecules. A fluorescence probe was design to validate this model by creating an Off/On system and determine the payload release location in situ. A process was optimized to synthetize the probe 8-(1-aminoethyl)-7-hydroxy-coumarin (1) through a reductive amination reaction in a microwave reactor with 61 % yield. A method to conjugate this probe to ABBA was also optimized, obtaining the iminoboronate in good yields in mild conditions. The iminoboronate model was studied regarding its stability in several simulated biological environments and each half-life time was determined, showing the conjugate is stable most of the cases except in tumour intracellular systems. The construction of folate-ABBA-coumarin bioconjugate have been made to complete this evaluation. The ability to be uptaken by a cancer cell through endocytosis process and the conjugation delivery of coumarin fluorescence payload are two features to hope for in this construct.

Aminobenzocoumarinylmehtyl esters as photoactive precursors for the release of butyric acid

The evaluation of the photorelease of a carboxylic acid drug, using butyric acid as a representative model, was carried out by using 7-amino-4-chloromethyl-2-oxo-2Hnaphtho[1,2-b] pyran, an aminobenzocoumarin, and its mono- and di-methylated or ethylated derivatives. This study was intended to improve the release of butyric acid from benzocoumarins by the addition of an amino group to the heterocycle by applying the knowledge of second-generation coumarinylmethyl-based photoremovable protecting groups. Photolysis studies were performed on the resultant ester cages by irradiation in a photochemical reactor at 254, 300, 350 and 419 nm, using methanol/HEPES buffer 80:20 solutions as solvent. The data obtained showed that these new fluorescent aminobenzocoumarins are superior to all the previously tested benzocoumarins with the same or different ring fusions. As well as the photolysis, the photophysics of the compounds were characterised by both steady state and time-resolved methods.

Comparison of oleate conversion under microaerophilic and anaerobic conditions

Excessive accumulation of Long Chain Fatty Acids (LCFA) in methanogenic bioreactors is the cause of process failure associated to a severe decrease in methane production. In particular, fast and persistent accumulation of palmitate is critical and still not elucidated. Aerobes or facultative anaerobes were detected in those reactors, raising new questions on LCFA biodegradation. To get insight into the influence of oxygen, two bioreactors were operated under microaerophilic and anaerobic conditions, with oleate at 1 and 4 gCOD/(L d). Palmitate accumulated up to 2 and 16 gCOD/L in the anaerobic and microaerophilic reactor, respectively, which shows the importance of oxygen in this conversion. A second experiment was designed to understand the dynamics of oleate to palmitate conversion. A CSTR and a PFR were assembled in series and fed with oleate under microaerophilic conditions. HRT from 6 to 24 h were applied in the CSTR, and 14 to 52 min in the PFR. In the PFR a biofilm was formed where palmitate accounted for 82% of total LCFA. Pseudomonas was the predominant genus (42 %) in this biofilm, highlighting the role of aerobic and facultative anaerobic bacteria in LCFA bioconversion.

Pró-fármacos fotoativáveis do péptido AAPV: síntese e avaliação da libertação controlada por luz

Dissertação de mestrado em Bioquímica Aplicada (área de especialização em Biomedicina)

Libertação fotocontrolada de moléculas bioativas a partir de conjugados de cumarinas

Dissertação de mestrado em Química Medicinal

Carbon materials as new generation of new electron shuttles for the anaerobic degradation of environmental xenobiotics

Tese de Doutoramento em Engenharia Química e Biológica

Remoção fotocatalítica de micropoluentes em meios porosos funcionalizados

Dissertação de mestrado integrado em Engenharia Civil

Valorization of agro-industrial wastes towards the production of rhamnolipids

In this work, oil mill wastewater (OMW), a residue generated during olive oil extraction, was evaluated as an inducer of rhamnolipid production. Using a medium containing as sole ingredients corn steep liquor (10%, v/v), sugarcane molasses (10%, w/v) and OMW (25%, v/v), Pseudomonas aeruginosa #112 produced 4.5 and 5.1 g of rhamnolipid per liter in flasks and reactor, respectively, with critical micelle concentrations as low as 13 mg/l. Furthermore, in the medium supplemented with OMW, a higher proportion of more hydrophobic rhamnolipid congeners was observed comparing with the same medium without OMW. OMW is a hazardous waste which disposal represents a serious environmental problem; therefore, its valorization as a substrate for the production of added-value compounds such as rhamnolipids is of great interest. This is the first report of rhamnolipid production using a mixture of these three agro-industrial by-products, which can be useful for the sustainable production of rhamnolipids.

Biodiscos : tratamiento biológico de contaminantes en efluentes líquidos

El creciente aumento de la población mundial ha generado un incremento de la demanda de agua con la consecuente disminución de su disponibilidad, situación que se ve agravada por la contaminación de recurso hídrico. La generación de aguas residuales es un hecho inevitable de toda actividad humana y los problemas asociados a las mismas causan deterioros ambientales y atentan contra la salud humana, debido a la ausencia de tratamientos adecuados y a los elevados costos de construcción de los mismos. La Universidad Católica de Córdoba a través de uno de sus Equipos de Investigación asume el compromiso de implementar un sistema que recupere el agua proveniente de los líquidos residuales generados en el campus universitario. Así, se diseña, construye e instala un prototipo que funciona como una innovadora planta compacta de remediación de líquidos residuales utilizando un reactor Biodiscos. Los Biodiscos o Contactores Biológicos Rotativos (RBC), forman parte de una de las tecnologías apropiadas y efi cientes para el tratamiento biológico-secundario de los líquidos residuales con alto contenido de materia orgánica biodegradable. La planta piloto utiliza como tratamiento primario un separador de grasas y un sistema decantador; como tratamiento secundario un Biodiscos y como tratamiento terciario un clarifi cador y dosifi cador de cloro. Biodiscos es un sistema biológico, aeróbico de cultivo fi jo, constituido por un reactor formado por una serie de discos, montados sobre un eje que gira a escasas revoluciones en una cuba semicilíndrica por donde circula el líquido residual; los discos están sumergidos un 40% en el líquido a tratar y sirven de soporte para que los microorganismos se adhieran y formen un fi lm llamado biopelícula, responsable de la depuración del efl uente, es decir, del consumo de los residuos sólidos presentes en el líquido. El líquido que egresa de esta planta de tratamiento es agua limpia, apta para diferentes usos, en el caso del campus universitario de la UCC será utilizado para riego ornamental del predio

Producción de diamante por CVD (Chemical Vapour Deposition)

A fines de la década del '60 un grupo de investigadores rusos pudo obtener diamante a partir de experimentos con reacciones en fase vapor a bajas presiones de los gases envueltos en el proceso. En 1976 Derjagin et al. mostraron que la nucleación de diamante es posible sobre sustratos de Cu y en 1982 Matsumoto demuestra que la nucleación y crecimiento continuo a bajas presiones de diamante es posible sobre diversos substratos. Las especiales propiedades del diamante (D): dureza, elevado punto de fusión, inercia química, así como elevada conductividad del calor, sonido y de señales ópticas, ubican a este material como una de las prioridades de desarrollo e investigación de grupos de excelencia en el mundo entero. (...) Objetivos Generales y Específicos: El objetivo de este proyecto se basa en la construcción de un reactor para CVD (Chemical Vapour Deposition) y de los elementos auxiliares necesarios para producir diamante sintético por este método. Determinando los parámetros que controlan el proceso: mezcla de gases adecuada, temperatura de substrato, temperatura del plasma, presión parcial de los gases, vacío necesario y otros. En la primera etapa de 2 años se priorizará la puesta a punto del método, para luego pasar al estudio de las diferentes aplicaciones tecnológicas necesarias para la región. Específicamente, en el tercer año se tratará de generar diamantes como recubrimientos para herramientas de corte, así como para trapanos de velocidad, aprovechando residuos para la industria de abrasivos. Los objetivos generales no se cirscuncriben sólo al hecho de montar un reactor en laboratorio para CVD, sino una vez encontrados los parámetros que gobiernan esta técnica, producir diamante sintético para aplicaciones en la industria de herramientas de corte, micrófonos y óptica. Otro objetivo general de importancia es la formación de recursos humanos en técnicas de vacío, ingeniería de superficie y tecnología de plasma a través del personal y de los estudiantes involucrados en el proyecto, así como los participantes en cátedras del Departamento de Mecánica. En cuanto a los objetivos específicos para los dos primeros años, es preparar, construir y poner a punto un reactor de laboratorio de filamento caliente (Hot filament) por tecnología de plasma tipo CVD para obtener diamante sintético a partir de gases.